• 한국분말야금학회:학술대회논문집
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• 한국분말야금학회 2006년도 Extended Abstracts of 2006 POWDER METALLURGY World Congress Part 1
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• pp.491-492
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• 2006

The horizontal high energy rotor ball mill ($Simoloyer^{(R)}$) is used to break and activate dry solids. It is used for dry-milling and in the vertical mount for wet-milling in leaching processes. Technical electric arc furnace (EAF) dust with high contents of zinc oxide, zinc ferrite and magnetite is efficiently separated by ambient temperature leaching. The process shows promise for industrial application

• 대한전자공학회:학술대회논문집
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• 대한전자공학회 2001년도 The 6th International Symposium of East Asian Resources Recycling Technology
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• pp.387-392
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• 2001

Kobe Steel, LTD. and Midrex Technologies Inc. jointly developed the FASTMET$\circledR$ process as a steel mill waste recycle technology in which the DRI product meets BF feed material or BOF/EAF feed material requirements. FASTMET(R) process turns value-less wastes into valuable DRI and sellable zinc oxide, and gives the solution for the steel mill wastes recycling from both economical and environmental viewpoints. During the development of the process, Laboratory, Pilot Plant and Demonstration Plant tests were carried out from 1990 to 1998. The first FASTMET(R) commercial plant began operation in April, 2000 and the second commercial plant started in April, 2001 Both commercial plants have proceeded successfully preying that FASTMET$\circledR$ is a suitable process for recycling steel mill waste and for producing DRI as an iron source.

• 대한전자공학회:학술대회논문집
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• 대한전자공학회 2001년도 The 6th International Symposium of East Asian Resources Recycling Technology
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• pp.437-442
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• 2001

In an integrated steel mill, zinc (Zn) inputs from raw materials and steel scrap are enriched in the dusts and sludges collected from gas and water cleaning systems. The reuse of these dusts and sludges must be controlled within certain limit to avoid Zn accumulation and related operational problems in blast furnace. An integrated system has been established at China Steel Corporation (CSC) to enhance the internal reuse of Zn-containing dust/sludge while keeping Zn input within control lim it. However. the performance of this system has not been very satisfactory until one and half years ago when a rationalization process was initiated. The essence of this rationalization process, the recent improvements in Zn control and dust and sludge reuse are reported and discussed.

• 자원리싸이클링
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• 제26권5호
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• pp.48-53
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• 2017

전기로 제강 공정에서 분진은 제강생산량의 1 ~ 2%가 발생하고 있으며, 분진 중에는 유가금속인 Zn과 Fe가 20 ~ 30% 정도 함유되어 있다. 전기로 배가스에 포함된 분진은 전기로 출구 덕트를 빠져나와 배가스를 완전연소하기 위한 연소탑과 냉각을 위한 냉각탑을 거쳐 Bag filter에 포집된다. 연소탑 하단에서 비중 차이에 의해 포집되는 분진은 전체 발생량의 15%에 해당하며 기존 Bag filter 분진보다 고가로 위탁처리 되고 있다. 본 연구는 연소탑 하단에 포집되는 분진의 유가금속 분리 회수에 대한 연구로서, 전기로 조업 시점과 분진의 입도에 따른 성분을 분석하여 유가금속의 함량 차이를 비교하였다. 본 연구 결과 전기로 조업 시점에 따른 영향 보다는 입도에 따라 Zn과 Fe의 함량에 큰 차이를 보였다.

• 자원리싸이클링
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• 제29권1호
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• pp.3-16
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• 2020

본 논문에서는 철강제조 프로세스, 철스크랩의 전처리와 미량 원소, 그리고 철강공정에서 발생하는 분진의 리사이클링 기술에 대해 고찰하였다. 철강은 인류가 가장 많이 사용하는 범용 금속으로, 2018년 기준 전세계 조강 생산량은 18억 톤을 초과하였다. 철을 리사이클링하면 철광석으로부터 환원하여 철강재를 얻는 것에 비하여 CO₂ 발생량은 약 42 % 수준이며, 에너지는 약 60 %를 절약할 수 있다. 철스크랩은 스크랩을 주원료 사용하는 전기로제강과 철광석을 주원료로 사용하는 전로 제강공정에서 리사이클링되고 있다. 철스크랩을 주원료로 사용하는 전기로 제강법은 스크랩을 예열하는 장치를 부가한 에너지 절약형으로 바뀌어 가고 있다. 철강 제조공정에서 발생하는 분진은 제철소 내에서 다양한 방법으로 리사이클링하여 철분과 아연 등을 회수하고 있다.

• 자원리싸이클링
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• 제3권2호
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• pp.9-16
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• 1994

본 연구에서는 제철소 전로 dust를 사용하여 일차보고의 기초적인 철분말의 회수에 이어 semi pilot 장치의 혼식 사이클론(wet cyclone)을 사용해서 고순도의 철분말을 회소하여 분말합금용(용접봉용 포함) 원료, 철분법 페수처리용 등으로 그 용도를 개발하고자 하였으며, 이를 통하여 다음과 같은 결론을 얻었다. 1. 광양제철소 EC dust를 vibration mill로 2분 동안 마광한 다음 혼식 사이클론에 분급하여 얻어진 철분말(+200 mesh. underflow)를 다시 아트리터에서 5분 동안 마광한 후 분급실험을 하여 고순도으 철분말(Total Fe 99.76%)을 47.66% 회수할 수 있었다. 2. 전로 dust에서 회수한 철분말은 +65 mesh : 36.16%, 65/100 : 24.43%, 100/200 : 26.68%, 200/270 : 12.64%의 입도분포를 가지고 있었으며, 모두 ${\alpha}$-Fe러 flake형을 보이고 있었다. 3. 재항 CF dust와 광양 EC dust에서 회수한 철분말을 가지고 동이온 제거실험을 한 결과, 철분말에 의해서 동이온이 99%이상 제거됨을 알 수 있었다. 4. 전로 dust를 적당시간 마광하여 혼식 사이클론에 의해 +270mesh(underflow)와 -270 mesh(overflow)로 입도로 분급한 후, -270 mesh 의 입도(산화철)는 폐수처리용 원료로 사용하고, +270mesh 의 입도(철분말)는 분말합금용(용접봉용 포함) 원료로 사용하는 것이 바람직하다.

• 한국환경과학회지
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• 제21권5호
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• pp.613-622
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• 2012

A pilot-scale pulse-jet bagfilter was designed, built and tested for the effects of four operating conditions (filtration velocity, inlet dust concentration, pulse pressure, and pulse interval time) on the total system pressure drop, using coke dust from a steel mill factory. Two models were used to predict the total pressure drop according to the operating conditions. These model parameters were estimated from the 180 experimental data points. The empirical model (EM) with filtration velocity, areal density, inlet dust concentration, pulse interval time and pulse pressure shows the best correlation coefficient (R=0.971) between experimental data and model predictions. The empirical model was used as it showed higher correlation coefficient (R=0.971) compared to that of the Multivariate linear regression(MLR) (R=0.961). The minimum pulse pressure predicted by empirical model (EM) was 5kg/$cm^2$.

• 한국환경과학회지
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• 제23권12호
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• pp.2045-2056
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• 2014

In this study, pressure drop was measured in the pulse jet bag filter without venturi on which 16 numbers of filter bags (Ø$140{\times}850{\ell}$) are installed according to operation condition(filtration velocity, inlet dust concentration, pulse pressure, and pulse interval) using coke dust from steel mill. The obtained 180 pressure drop test data were used to predict pressure drop with multiple regression model so that pressure drop data can be used for effective operation condition and as basic data for economical design. The prediction results showed that when filtration velocity was increased by 1%, pressure drop was increased by 2.2% which indicated that filtration velocity among operation condition was attributed on the pressure drop the most. Pressure was dropped by 1.53% when pulse pressure was increased by 1% which also confirmed that pulse pressure was the major factor affecting on the pressure drop next to filtration velocity. Meanwhile, pressure drops were found increased by 0.3% and 0.37%, respectively when inlet dust concentration and pulse interval were increased by 1% implying that the effects of inlet dust concentration and pulse interval were less as compared with those changes of filtration velocity and pulse pressure. Therefore, the larger effect on the pressure drop the pulse jet bag filter was found in the order of filtration velocity($V_f$), pulse pressure($P_p$), inlet dust concentration($C_i$), pulse interval($P_i$). Also, the prediction result of filtration velocity, inlet dust concentration, pulse pressure, and pulse interval which showed the largest effect on the pressure drop indicated that stable operation can be executed with filtration velocity less than 1.5 m/min and inlet dust concentration less than $4g/m^3$. However, it was regarded that pulse pressure and pulse interval need to be adjusted when inlet dust concentration is higher than $4g/m^3$. When filtration velocity and pulse pressure were examined, operation was possible regardless of changes in pulse pressure if filtration velocity was at 1.5 m/min. If filtration velocity was increased to 2 m/min. operation would be possible only when pulse pressure was set at higher than $5.8kgf/cm^2$. Also, the prediction result of pressure drop with filtration velocity and pulse interval showed that operation with pulse interval less than 50 sec. should be carried out under filtration velocity at 1.5 m/min. While, pulse interval should be set at lower than 11 sec. if filtration velocity was set at 2 m/min. Under the conditions of filtration velocity lower than 1 m/min and high pulse pressure higher than $7kgf/cm^2$, though pressure drop would be less, in this case, economic feasibility would be low due to increased in installation and operation cost since scale of dust collection equipment becomes larger and life of filtration bag becomes shortened due to high pulse pressure.

• 한국환경과학회지
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• 제19권4호
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• pp.437-446
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• 2010

The pressure drop through pulse air jet-type bag filter is one of the most important factors on the operating cost of bagfilter houses. In this study, the pilot-scale pulse air jet-type bag filter with about 6 m2 filtration area was designed and tested for investigating the effects of the four operating conditions on the total pressure drop, using the coke dust collected from a steel mill factory. When the face velocity is higher than 2 m/min, it is not applicable to on-spot due to the increase of power expenses resulting from a high-pressure drop, and thus, 1.5 m/min is considered to be reasonable. The regression analysis results show that the degree of effects of independent parameters is a order of face velocity > concentration > time > pressure. The results of SPSS answer tree analysis also reveal that the operation time affects the pressure drop greatly in case of 1 m/min of face velocity, while the inlet concentration affects the pressure drop in case of face velocity more than 1.5 m/min.